US6080562A - HV/HB copolymer production - Google Patents

HV/HB copolymer production Download PDF

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Publication number
US6080562A
US6080562A US07/949,524 US94952492A US6080562A US 6080562 A US6080562 A US 6080562A US 94952492 A US94952492 A US 94952492A US 6080562 A US6080562 A US 6080562A
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microorganism
amino acid
substrate
cultivated
monomer units
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US07/949,524
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David Byrom
Alexander Steinbuchel
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CJ CheilJedang Corp
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Monsanto Co
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Assigned to IMPERIAL CHEMICAL INDUSTRIES PLC reassignment IMPERIAL CHEMICAL INDUSTRIES PLC ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: STEINBUCKEL, ALEXANDER, BYROM, DAVID
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Assigned to METABOLIX, INC. reassignment METABOLIX, INC. RELEASE BY SECURED PARTY (SEE DOCUMENT FOR DETAILS). Assignors: MONSANTO COMPANY
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Assigned to METABOLIX, INC. reassignment METABOLIX, INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: MONSANTO COMPANY
Assigned to METABOLIX, INC. reassignment METABOLIX, INC. ADDRESS CHANGE Assignors: METABOLIX, INC.
Assigned to CJ RESEARCH CENTER LLC reassignment CJ RESEARCH CENTER LLC ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: METABOLIX, INC.
Assigned to CJ CHEILJEDANG CORPORATION reassignment CJ CHEILJEDANG CORPORATION ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: CJ RESEARCH CENTER LLC
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/02Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds
    • C08G63/06Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds derived from hydroxycarboxylic acids
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P7/00Preparation of oxygen-containing organic compounds
    • C12P7/62Carboxylic acid esters
    • C12P7/625Polyesters of hydroxy carboxylic acids
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S435/00Chemistry: molecular biology and microbiology
    • Y10S435/8215Microorganisms
    • Y10S435/822Microorganisms using bacteria or actinomycetales
    • Y10S435/829Alcaligenes

Definitions

  • This invention relates to a process for the production of HV/HB copolymers and for microorganisms for use in such a process.
  • strains of the species Rhodococcus capable of producing, and accumulating, HV/HB copolymers have the characteristic that they overproduce at least one amino acid, specifically at least one of methionine and preferably isoieucine or valine, and that these overproduced amino acids are metabolised to propionyl CoA, and thence to the required HV monomer units.
  • microorganisms capable of producing, and accumulating, HV/HB copolymers which comprises providing within a suitable microorganism the ability to overproduce at least one of isoleucine, methionine and valine. Such microorganisms may then be used in a general microbiclogical process for the production of HV/HB copolymers, when provided with suitable substrate for example comprising glucose, or a compound metabolisable to glucose.
  • the invention comprises a method of producing a microorganism capable of sythesizing HV/HB copolymer when cultivated on a substrate containing a component from which the microorganism can synthesise both HV and HB monomer units from a first microorganism which is capable of metabolising the substrate to acetyl CoA and is also capable of degrading an amino acid selected from methionine, valine and isoleucine to propionyl CoA which method comprises when said first microorganism is capable of synthesising and polymerising HB monomer units when cultivated on said substrate but is not capable of amino acid overproduction, inducing overproduction of said amino acid in said first microorganism, and when said first microorganism is not capable of synthesising and polymerising HB monomer units when cultivated on said substrate but is capable of overproducing said amino acid, transferring to said first microorganism the genetic information necessary for it to synthesise and polymerise HB monomer units when cultivated on said substrate from
  • the microorganism is preferably a strain of Alcaligenes.
  • Alcaligenes eutrophus NCIMB 11599, and NICMB 40124 are examples of such strains.
  • NCIMB 40124 is preferred in that in this strain the use of propionyl CoA for growth is blocked, thereby giving rise to improved efficiency of HV/HB copolymer production, and also higher percentages of HV monomer in the copolymer.
  • the method for preparing microorganisms in which amino acid overproduction is apparent may include exposure of the microorganism to amino acid analogues such as amino butyric acid, and norvaline.
  • amino acid analogues such as amino butyric acid, and norvaline.
  • the required mutations may be spontaneous, or may be induced by the use of suitable mutagenic agents such as UV light, ethane methane sulphonate and N-nitroso-guanidine.
  • the microorganism produced according to the method of the present invention may be cultivated, in the general microbiological process, on a substrate in which the component from which the monomer units are synthesised is glucose, or a compound metabolisable to glucose.
  • the component is one or more of glucose, fructose, acetate, lactate, ethanol or derivatives thereof.
  • Alcaligenes eutrophus strain NCIMB 40124 was used as the initial strain which, by a mutation process, gave rise to an amino acid overproducing mutant.
  • Alcaligenes eutrophus NCIMB 40124 was grown on glucose mineral salts medium for approximately 16 hours at 30° C., until an optical density of greater than 1 at 640 ⁇ m was reached.
  • the subcultures of the colonies for Example 1 were cultivated on typical media which contained sources of nitrogen (ammonium salts), carbon (glucose), and trace elements such as phosphate, sulphate and magnesium.
  • the cultivation was allowed to proceed to nutrient limitation, specifically nitrogen limitation as used in established HB copolymer production. Those cultures which accumulated HV/HB copolymer were regarded as positive. In particular Alcaligenes eutrophus strain PS-101 was isolated.
  • Alcaligenes eutrophus strain PS-101 was further cultivated under copolymer accumulating conditions on a medium in which glucose was the sole carbon source.
  • Example 3 was repeated except that Alcaligenes eutrophus strain NCIMB 40124 was used instead of mutant strain PS-101.
  • Strain NCIMB 40386 was produced from Alcaligenes eutrophus strain NCIMB 40124 by the following means:
  • a single colony of NCIMB 40124 was inoculated into the medium listed in Table 1 containing 1% glucose.
  • the inoculated medium was incubated by shaking at 180 rpm and at a temperature of 28° C. until the mid logarithmic phase.
  • the cells were harvested by centrifugation, washed with 0.85% sodium chloride solution and re-suspended in 0.85% sodium chloride solution and transferred to a glass petri dish.
  • the cells were exposed to UV light to achieve a 99% kill and then inoculated into the medium listed in Table 1 containing 1% glucose.
  • the inoculated medium was incubated by shaking at 180 rpm and at 28° C. for 16 hours in the dark to allow expression of the mutations.
  • the resulting population was spread onto agar plates containing the medium listed in Table 1 and 500 ⁇ g/ml ⁇ - amino-butyric acid. The plates were incubated for seven days at 28° C. Resistant colonies were selected which showed halos of satellite growth: the halo indicated that the resistant colonies were excreting a substance which relieved the inhibition for the surrounding sensitive cells. This selection produced strain NCIMB 40386 with the ability to produce and accumulate HB/HV copolymer when provided with glucose as shown by Example 6.
  • the growth medium listed in Table 1 containing 1% glucose and 500 ⁇ g/ml ⁇ - aminobutyric acid was inoculated with a culture of Alcaligenes eutrophus NCIMB 40386 produced as described in Example 5.
  • the inoculated medium was shaken using a stirrer speed of 180 rpm and (2") approximately 50 mm (2 inches) throw at a temperature of 28° C. for 24 hours.
  • the cells were harvested by centrifugation, washed with 0.85% sodium chloride solution and then resuspended in the growth medium listed in Table 1 containing 1% glucose and replacing the phosphate buffer with 0.5 m Hepes buffer.
  • the medium was incubated shaking at 180 rpm, (2") approximately 50 mm (2 inches) throw, at a temperature of 28° C. for 48 hours.
  • the cells were harvested by centrifugation, washed with 0.85% sodium chloride solution and freeze dried.
  • the freeze dried cells were ground to a fine powder with a pestle and mortar. 10 g of cells were refluxed with 500 mls chloroform for one hour.
  • the resulting solution was filtered under vacuum and the polymer was recovered by precipitation with methanol and water.
  • the polymer solution was slowly added, with mixing to a solution+consisting of 2 litres water and 500 mls distilled water.
  • the polymer precipitate was then filtered and dried for 24 hours at 80° C.
  • Freeze dried cells were prepared for analysis using High Performance Liquid Chromatography (HPLC) by extraction in 55% perchloric acid and neutralised with 20% potassium hydroxide.
  • HPLC High Performance Liquid Chromatography
  • Alcaligenes eutrophus strain H16 a widely available micro-organism available for example from NCIMB as NCIMB 10442 was used as the initial strain in a mutation process which gave rise to amino acid overproducing mutants.
  • Algaligenes eutrophus strain H16 was grown on mineral salts medium containing 1% fructose and the resultant cells subjected to UV mutagenesis by exposure to sufficient UV dose to give between 90 to 99% kill.
  • the survivors were inoculated into nutrient broth (0.8% Oxoid) and were shaken whilst being incubated overnight in the dark at a temperature of 28° C. to allow expression of the mutations.
  • the colistine technique was used to enrich the population of mutants for auxotrophs.
  • Cells were incubated in the presence of 50 ⁇ g.ml -1 colistine for 10 hours. Dilutions of the survivors were plated onto complete medium agar (0.8% nutrient broth and 01.5% NaCl).
  • Replica plating to fructose mineral salts agar was used to identify auxotrophic colonies. By this means the mutant Alcaligenes eutrophus H16-G131 was isolated. The mutant was found to require isoleucine (Reh M and Schlegel H G. 1969. Arch. Mikrobiol. 67. 99-109).
  • Colonies of Alcaligenes eutrophus H16-R3 were inocculated into 10 mls of nutrient broth (oxoid) and a shake flask preculture was incubated overnight at 30° C. This preculture was then used to inoculate 300 mls of 1% fructose-mineral salts medium containing only 0.05% ammonium chloride in a 1 liter flask. The flask was incubated with shaking at 30° C.
  • PHA polyhydroxyalkanoate
  • NCIMB means NCIMB Limited, 23 Machar Drive, Aberdeen, Scotland, UK AB2 1RY. NCIMB 40386 was deposited on Mar. 20, 1991 with NCIMB.
  • Alcaligenes eutrophus H16-R3 is deposited as DSM 6525 with Deutsche Sammlung von Mikroorganismen and Zellkulturen (DSM), Mascheroder Weg 1b, D-3300 Braunschweig, Germany on May 15, 1991.
  • DSM Deutsche Sammlung von Mikroorganismen and Zellkulturen

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Zoology (AREA)
  • Health & Medical Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Biochemistry (AREA)
  • General Engineering & Computer Science (AREA)
  • Microbiology (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Medicinal Chemistry (AREA)
  • Biotechnology (AREA)
  • Polymers & Plastics (AREA)
  • General Chemical & Material Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Organic Insulating Materials (AREA)
  • Polyesters Or Polycarbonates (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)
  • Piezo-Electric Transducers For Audible Bands (AREA)
  • Saccharide Compounds (AREA)
US07/949,524 1990-05-25 1991-05-24 HV/HB copolymer production Expired - Lifetime US6080562A (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
GB9011777 1990-05-25
GB909011777A GB9011777D0 (en) 1990-05-25 1990-05-25 Hv/hb copolymer production
PCT/EP1991/000978 WO1991018995A1 (en) 1990-05-25 1991-05-24 Hv/hb copolymer production

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US6080562A true US6080562A (en) 2000-06-27

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US07/949,524 Expired - Lifetime US6080562A (en) 1990-05-25 1991-05-24 HV/HB copolymer production

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US (1) US6080562A (de)
EP (1) EP0535012B1 (de)
JP (1) JPH05506784A (de)
AT (1) ATE127846T1 (de)
AU (1) AU652942B2 (de)
CA (1) CA2083695C (de)
DE (1) DE69113041T2 (de)
GB (1) GB9011777D0 (de)
WO (1) WO1991018995A1 (de)

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20040232355A1 (en) * 2003-05-21 2004-11-25 Asm Japan K.K. Gas-shield electron-beam gun for thin-film curing application
US20100112654A1 (en) * 2008-09-10 2010-05-06 Burk Mark J Microorganisms for the production of 1,4-butanediol
US20110003355A1 (en) * 2009-06-04 2011-01-06 Genomatica, Inc Process of separating components of a fermentation broth
US7947483B2 (en) 2007-08-10 2011-05-24 Genomatica, Inc. Methods and organisms for the growth-coupled production of 1,4-butanediol
US20110129899A1 (en) * 2009-10-13 2011-06-02 Robert Haselbeck Microorganisms for the production of 1,4-butanediol, 4-hydroxybutanal, 4-hydroxybutyryl-coa, putrescine and related compounds, and methods related thereto
US20110201089A1 (en) * 2010-02-23 2011-08-18 Burgard Anthony P Methods for increasing product yields
US20110217742A1 (en) * 2009-11-25 2011-09-08 Jun Sun Microorganisms and methods for the coproduction 1,4-butanediol and gamma-butyrolactone
US8067214B2 (en) 2007-03-16 2011-11-29 Genomatica, Inc. Compositions and methods for the biosynthesis of 1,4-butanediol and its precursors
US8129169B2 (en) 2009-06-04 2012-03-06 Genomatica, Inc. Microorganisms for the production of 1,4-butanediol and related methods
US8445244B2 (en) 2010-02-23 2013-05-21 Genomatica, Inc. Methods for increasing product yields
US9677045B2 (en) 2012-06-04 2017-06-13 Genomatica, Inc. Microorganisms and methods for production of 4-hydroxybutyrate, 1,4-butanediol and related compounds

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB9223709D0 (en) * 1992-11-12 1992-12-23 Ici Plc Process for the separation of protein from microorganisms
AU5676394A (en) * 1992-11-20 1994-06-22 Agracetus, Inc. Transgenic cotton plants producing heterologous bioplastic
US5958745A (en) * 1996-03-13 1999-09-28 Monsanto Company Methods of optimizing substrate pools and biosynthesis of poly-β-hydroxybutyrate-co-poly-β-hydroxyvalerate in bacteria and plants
US6946588B2 (en) 1996-03-13 2005-09-20 Monsanto Technology Llc Nucleic acid encoding a modified threonine deaminase and methods of use
US5959179A (en) * 1996-03-13 1999-09-28 Monsanto Company Method for transforming soybeans
GB9605704D0 (en) * 1996-03-19 1996-05-22 Zeneca Ltd Microorganisms and processes using them
US6562603B2 (en) * 2000-08-04 2003-05-13 E. I. Du Pont De Nemours And Company 3-hydroxycarboxylic acid production and use in branched polymers

Citations (5)

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US4477654A (en) * 1981-07-07 1984-10-16 Imperial Chemical Industries Plc 3-Hydroxybutyrate polymers
EP0204442A2 (de) * 1985-05-28 1986-12-10 Imperial Chemical Industries Plc Copolymerherstellung
EP0288908A2 (de) * 1987-04-28 1988-11-02 Mitsubishi Gas Chemical Company, Inc. Verfahren zur Herstellung eines D-(-)-3-Hydroxybutyrat- und D-(-)-3-Hydroxyvalerat-Einheiten enthaltenden Zufallscopolymers
US4876331A (en) * 1987-08-18 1989-10-24 Mitsubishi Kasei Corporation Copolyester and process for producing the same
US5126255A (en) * 1989-05-02 1992-06-30 Imperial Chemical Industries Plc Copolymer production

Family Cites Families (1)

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GB8927794D0 (en) * 1989-12-08 1990-02-14 Ici Plc Copolymer production

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4477654A (en) * 1981-07-07 1984-10-16 Imperial Chemical Industries Plc 3-Hydroxybutyrate polymers
EP0204442A2 (de) * 1985-05-28 1986-12-10 Imperial Chemical Industries Plc Copolymerherstellung
EP0288908A2 (de) * 1987-04-28 1988-11-02 Mitsubishi Gas Chemical Company, Inc. Verfahren zur Herstellung eines D-(-)-3-Hydroxybutyrat- und D-(-)-3-Hydroxyvalerat-Einheiten enthaltenden Zufallscopolymers
US4997909A (en) * 1987-04-28 1991-03-05 Mitsubishi Gas Chemical Company, Inc. Random copolymer comprising D-(-)-3-hydroxybutyrate units and D-(-)-3-hydroxyvalerate, and process for production thereof
US4876331A (en) * 1987-08-18 1989-10-24 Mitsubishi Kasei Corporation Copolyester and process for producing the same
US5126255A (en) * 1989-05-02 1992-06-30 Imperial Chemical Industries Plc Copolymer production

Cited By (38)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20040232355A1 (en) * 2003-05-21 2004-11-25 Asm Japan K.K. Gas-shield electron-beam gun for thin-film curing application
US7012268B2 (en) 2003-05-21 2006-03-14 Asm Japan K.K. Gas-shield electron-beam gun for thin-film curing application
US9487803B2 (en) 2007-03-16 2016-11-08 Genomatica, Inc. Compositions and methods for the biosynthesis of 1,4-butanediol and its precursors
US8889399B2 (en) 2007-03-16 2014-11-18 Genomatica, Inc. Compositions and methods for the biosynthesis of 1,4-butanediol and its precursors
US8357520B2 (en) 2007-03-16 2013-01-22 Genomatica, Inc. Compositions and methods for the biosynthesis of 1,4-butanediol and its precursors
US8067214B2 (en) 2007-03-16 2011-11-29 Genomatica, Inc. Compositions and methods for the biosynthesis of 1,4-butanediol and its precursors
US11371046B2 (en) 2007-03-16 2022-06-28 Genomatica, Inc. Compositions and methods for the biosynthesis of 1,4-butanediol and its precursors
US8969054B2 (en) 2007-03-16 2015-03-03 Genomatica, Inc. Compositions and methods for the biosynthesis of 1,4-butanediol and its precursors
US7947483B2 (en) 2007-08-10 2011-05-24 Genomatica, Inc. Methods and organisms for the growth-coupled production of 1,4-butanediol
US8470582B2 (en) 2007-08-10 2013-06-25 Genomatica, Inc. Methods and organisms for the growth-coupled production of 1,4-butanediol
US7858350B2 (en) 2008-09-10 2010-12-28 Genomatica, Inc. Microorganisms for the production of 1,4-butanediol
US20110159572A1 (en) * 2008-09-10 2011-06-30 Genomatica, Inc. Microorganisms for the production of 1,4-butanediol
US9175297B2 (en) 2008-09-10 2015-11-03 Genomatica, Inc. Microorganisms for the production of 1,4-Butanediol
US20100112654A1 (en) * 2008-09-10 2010-05-06 Burk Mark J Microorganisms for the production of 1,4-butanediol
US8129156B2 (en) 2008-09-10 2012-03-06 Genomatica, Inc. Microorganisms for the production of 1,4-butanediol
US8178327B2 (en) 2008-09-10 2012-05-15 Genomatica, Inc. Microorganisms for the production of 1,4-butanediol
US8597918B2 (en) 2009-06-04 2013-12-03 Genomatica, Inc. Process of separating components of a fermentation broth
US20110003355A1 (en) * 2009-06-04 2011-01-06 Genomatica, Inc Process of separating components of a fermentation broth
US9434964B2 (en) 2009-06-04 2016-09-06 Genomatica, Inc. Microorganisms for the production of 1,4-butanediol and related methods
US10273508B2 (en) 2009-06-04 2019-04-30 Genomatica, Inc. Microorganisms for the production of 1,4-butanediol and related methods
US8129169B2 (en) 2009-06-04 2012-03-06 Genomatica, Inc. Microorganisms for the production of 1,4-butanediol and related methods
US11401534B2 (en) 2009-06-04 2022-08-02 Genomatica, Inc. Microorganisms for the production of 1,4- butanediol and related methods
US20110129899A1 (en) * 2009-10-13 2011-06-02 Robert Haselbeck Microorganisms for the production of 1,4-butanediol, 4-hydroxybutanal, 4-hydroxybutyryl-coa, putrescine and related compounds, and methods related thereto
US8377666B2 (en) 2009-10-13 2013-02-19 Genomatica, Inc. Microorganisms for the production of 1,4-butanediol, 4-hydroxybutanal, 4-hydroxybutyryl-coa, putrescine and related compounds, and methods related thereto
US8377667B2 (en) 2009-10-13 2013-02-19 Genomatica, Inc. Microorganisms for the production of 1,4-butanediol, 4-hydroxybutanal, 4-hydroxybutyryl-CoA, putrescine and related compounds, and methods related thereto
US20110229946A1 (en) * 2009-10-13 2011-09-22 Genomatica, Inc. Microorganisms for the production of 1,4-butanediol, 4-hydroxybutanal, 4-hydroxybutyryl-coa, putrescine and related compounds, and methods related thereto
US20110217742A1 (en) * 2009-11-25 2011-09-08 Jun Sun Microorganisms and methods for the coproduction 1,4-butanediol and gamma-butyrolactone
US9222113B2 (en) 2009-11-25 2015-12-29 Genomatica, Inc. Microorganisms and methods for the coproduction 1,4-butanediol and gamma-butyrolactone
US8530210B2 (en) 2009-11-25 2013-09-10 Genomatica, Inc. Microorganisms and methods for the coproduction 1,4-butanediol and gamma-butyrolactone
US9988656B2 (en) 2009-11-25 2018-06-05 Genomatica, Inc. Microorganisms and methods for the coproduction 1,4-butanediol and gamma-butyrolactone
US10662451B2 (en) 2009-11-25 2020-05-26 Genomatica, Inc. Microorganisms and methods for the coproduction 1,4-butanediol and gamma-butyrolactone
US8637286B2 (en) 2010-02-23 2014-01-28 Genomatica, Inc. Methods for increasing product yields
US8445244B2 (en) 2010-02-23 2013-05-21 Genomatica, Inc. Methods for increasing product yields
US8048661B2 (en) 2010-02-23 2011-11-01 Genomatica, Inc. Microbial organisms comprising exogenous nucleic acids encoding reductive TCA pathway enzymes
US20110201089A1 (en) * 2010-02-23 2011-08-18 Burgard Anthony P Methods for increasing product yields
US9677045B2 (en) 2012-06-04 2017-06-13 Genomatica, Inc. Microorganisms and methods for production of 4-hydroxybutyrate, 1,4-butanediol and related compounds
US11085015B2 (en) 2012-06-04 2021-08-10 Genomatica, Inc. Microorganisms and methods for production of 4-hydroxybutyrate, 1,4-butanediol and related compounds
US11932845B2 (en) 2012-06-04 2024-03-19 Genomatica, Inc. Microorganisms and methods for production of 4-hydroxybutyrate, 1,4-butanediol and related compounds

Also Published As

Publication number Publication date
CA2083695C (en) 2002-01-08
CA2083695A1 (en) 1991-11-26
ATE127846T1 (de) 1995-09-15
AU652942B2 (en) 1994-09-15
DE69113041T2 (de) 1996-02-29
WO1991018995A1 (en) 1991-12-12
JPH05506784A (ja) 1993-10-07
AU7970891A (en) 1991-12-31
EP0535012B1 (de) 1995-09-13
GB9011777D0 (en) 1990-07-18
EP0535012A1 (de) 1993-04-07
DE69113041D1 (de) 1995-10-19

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